Optimization approach for the analytical design of an industrial PI controller for the optimal regulatory control of first order processes under operational constraints

Abstract In this paper, an optimization-based approach for the closed-form design of an industrial proportional-integral (PI) controller was proposed for the optimal regulatory control of first order process under three typical operational constraints. An ingenious parameterization with Lagrangian multiplier method was used to convert the constrained optimal control problem in the time domain to an unconstrained optimization problem to derive an analytical solution for the optimal regulatory control. Three typical operational constraints could be taken into account in the controller design stage, explicitly. The proposed analytical design method required no complicated optimization steps and guaranteed global optimal closed-loop performance and stability. The proposed analytical approach also provides useful insights into the optimal controller design and analysis. A practical and facile procedure for designing optimal PI parameters and a feasible constraint set was also proposed.

[1]  Khalid Alhumaizi,et al.  Temperature Control of Ethylene to Butene-1 Dimerization Reactor , 2000 .

[2]  C. Liou,et al.  The effect of nonideal mixing on input multiplicity in a CSTR , 1991 .

[3]  Moonyong Lee,et al.  Analytical design of proportional-integral controllers for the optimal control of first-order processes with operational constraints , 2013, Korean Journal of Chemical Engineering.

[4]  M. Lee,et al.  Implement a constrained optimal control in a conventional level controller: Part 2 , 2010 .

[5]  Moonyong Lee,et al.  Optimization Based Approach for Industrial PI Controller Design for Optimal Servo Control of Integrating Process with Constraints , 2011 .

[6]  S. Costanzo,et al.  Improve vacuum tower revamp projects: A 'balanced approach' investigates separation of vapor and liquids in the flash zone/wash section design , 2010 .

[7]  Yi Xiong,et al.  Unknown disturbance inputs estimation based on a state functional observer design , 2003, Autom..

[8]  M. Chidambaram,et al.  Control of unstable processes with two RHP poles, a zero and time delay , 2006 .

[9]  Wang Yang,et al.  Industrial application of a nonlinear model predictive control to polymerization reactors , 2001 .

[10]  M. Chidambaram,et al.  Enhanced Control of Unstable Cascade Processes with Time Delays Using a Modified Smith Predictor , 2009 .

[11]  Panagiotis D. Christofides,et al.  Nonlinear control of particulate processes , 1999 .

[12]  Moonyong Lee,et al.  Analytical design of a proportional-integral controller for constrained optimal regulatory control of inventory loop , 2008 .

[13]  Pramod Agrawal,et al.  Analyses of various control schemes for continuous bioreactors , 1984 .

[14]  Moonyong Lee,et al.  CONSTRAINED OPTIMAL CONTROL OF LIQUID LEVEL LOOP USING A CONVENTIONAL PROPORTIONAL-INTEGRAL CONTROLLER , 2009 .

[15]  A. Vyas Performing correct initial blowdown calculations: These guidelines can help determine peak flowrate , 2010 .